BR9909460A - Catalyst and process for converting methanol to hydrocarbons - Google Patents

Catalyst and process for converting methanol to hydrocarbons

Info

Publication number
BR9909460A
BR9909460A BR9909460-6A BR9909460A BR9909460A BR 9909460 A BR9909460 A BR 9909460A BR 9909460 A BR9909460 A BR 9909460A BR 9909460 A BR9909460 A BR 9909460A
Authority
BR
Brazil
Prior art keywords
catalyst
methanol
temperature
hydrocarbons
dimethylbutane
Prior art date
Application number
BR9909460-6A
Other languages
Portuguese (pt)
Inventor
Stephen Harold Brown
Larry Arthur Green
Mark Fischer Mathias
David Harold Olson
Robert Adams Ware
William Alois Weber
Original Assignee
Mobil Oil Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mobil Oil Corp filed Critical Mobil Oil Corp
Publication of BR9909460A publication Critical patent/BR9909460A/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/061—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing metallic elements added to the zeolite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/005—Mixtures of molecular sieves comprising at least one molecular sieve which is not an aluminosilicate zeolite, e.g. from groups B01J29/03 - B01J29/049 or B01J29/82 - B01J29/89
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
    • B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • B01J29/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
    • C07C2/86—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon
    • C07C2/862—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only oxygen as hetero-atoms
    • C07C2/864—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation between a hydrocarbon and a non-hydrocarbon the non-hydrocarbon contains only oxygen as hetero-atoms the non-hydrocarbon is an alcohol
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/36—Steaming
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/40—Special temperature treatment, i.e. other than just for template removal
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/30—After treatment, characterised by the means used
    • B01J2229/42—Addition of matrix or binder particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/82—Phosphates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • C07C2527/14—Phosphorus; Compounds thereof
    • C07C2527/16—Phosphorus; Compounds thereof containing oxygen
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2529/00—Catalysts comprising molecular sieves
    • C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
    • C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
    • C07C2529/40—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/40—Ethylene production

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Patente de Invenção: <B>"CATALISADOR E PROCESSO PARA CONVERSãO DE METANOL A HIDROCARBONETOS"<D>. São fornecidos um catalisador e um processo para a conversão de metanol ou de dimetil éter a um produto que contenha C~ 2~ e C~ 4~ olefinas. O catalisador compreende um material cristalino poroso que tem um Parâmetro de Difusão para 2,2-dimetilbutano de 0,1-20 s^ -1^ quando medido a uma temperatura de 120°C e uma pressão de 2,2-dimetilbutano de 60 torr (8 kPa). Além disso, o catalisador é caracterizado por uma estabilidade hidrotérmica tal que, após tratamento com vapor d'água do catalisador a 1025°C durante 45 minutos em vapor d'água de 1 atmosfera, o catalisador exibe uma atividade de conversão de metanol de pelo menos 50% quando em contato com metanol a uma pressão parcial de metanol de 1 atmosfera, uma temperatura de 430°C e 0,5 WHSV. O material cristalino poroso é de preferência uma zeólita do poro médio, particularmente ZSM-5, que contém fósforo e que foi tratada rigorosamente a uma temperatura de pelo menos 950°C.Invention Patent: <B> "CATALYST AND PROCESS FOR CONVERSION OF METHANOL TO HYDROCARBONS" <D>. A catalyst and a process for converting methanol or dimethyl ether to a product containing C ~ 2 ~ and C ~ 4 ~ olefins are provided. The catalyst comprises a porous crystalline material that has a Diffusion Parameter for 2,2-dimethylbutane of 0,1-20 s ^ -1 ^ when measured at a temperature of 120 ° C and a pressure of 2,2-dimethylbutane of 60 torr (8 kPa). In addition, the catalyst is characterized by a hydrothermal stability such that, after treatment with water vapor from the catalyst at 1025 ° C for 45 minutes in water vapor from 1 atmosphere, the catalyst exhibits a methanol conversion activity of at least minus 50% when in contact with methanol at a methanol partial pressure of 1 atmosphere, a temperature of 430 ° C and 0.5 WHSV. The porous crystalline material is preferably a mid-pore zeolite, particularly ZSM-5, which contains phosphorus and which has been rigorously treated at a temperature of at least 950 ° C.

BR9909460-6A 1998-04-06 1999-04-01 Catalyst and process for converting methanol to hydrocarbons BR9909460A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US09/055,478 US6048816A (en) 1996-10-02 1998-04-06 Catalyst and process for converting methanol to hydrocarbons
PCT/US1999/007320 WO1999051549A1 (en) 1998-04-06 1999-04-01 Catalyst and process for converting methanol to hydrocarbons

Publications (1)

Publication Number Publication Date
BR9909460A true BR9909460A (en) 2000-12-12

Family

ID=21998106

Family Applications (1)

Application Number Title Priority Date Filing Date
BR9909460-6A BR9909460A (en) 1998-04-06 1999-04-01 Catalyst and process for converting methanol to hydrocarbons

Country Status (11)

Country Link
US (1) US6048816A (en)
EP (1) EP1073614A4 (en)
JP (1) JP2002510660A (en)
AR (1) AR015265A1 (en)
AU (1) AU764570B2 (en)
BR (1) BR9909460A (en)
CA (1) CA2327688A1 (en)
ID (1) ID29381A (en)
MX (1) MX213108B (en)
NO (1) NO20005020L (en)
WO (1) WO1999051549A1 (en)

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US6472569B1 (en) * 1999-04-16 2002-10-29 Phillips Petroleum Company Silicoaluminophosphate material, a method of making such improved material and the use thereof in the conversion of oxygenated hydrocarbons to an olefin and/or an ether
US6613951B1 (en) 1999-09-23 2003-09-02 Mobil Oil Corporation Process for converting methanol to olefins
IT1314190B1 (en) * 1999-10-18 2002-12-06 Eni Spa PROCESS FOR PREPARING 2,6-DIMETHYLNAPHTHALENE
KR20020061011A (en) * 1999-12-28 2002-07-19 코닝 인코포레이티드 Zeolite/alumina catalyst support compositions and method of making the same
US6743747B1 (en) * 2000-02-24 2004-06-01 Exxonmobil Chemical Patents Inc. Catalyst pretreatment in an oxgenate to olefins reaction system
US6797851B2 (en) * 2001-08-30 2004-09-28 Exxonmobil Chemical Patents Inc. Two catalyst process for making olefin
US6823684B2 (en) 2002-02-08 2004-11-30 Tim Allan Nygaard Jensen System and method for cooling air
US6638892B1 (en) * 2002-04-18 2003-10-28 Conocophillips Company Syngas conversion and catalyst system employed therefor
US20040097769A1 (en) * 2002-11-14 2004-05-20 Ou John D. Y. Para-xylene production process employing in-situ catalyst selectivation
US7084318B2 (en) * 2003-08-01 2006-08-01 Saudi Basic Industries Corporation Toluene methylation process
US7060864B2 (en) * 2003-09-30 2006-06-13 Saudi Basic Industries Corporation Toluene methylation process
US7060644B2 (en) * 2004-01-08 2006-06-13 Saudi Basic Industries Corporation Aromatic alkylation catalyst and method
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KR101548755B1 (en) 2007-08-13 2015-08-31 사우디 베이식 인더스트리즈 코포레이션 Process for converting aliphatic oxygenates to aromatics
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Also Published As

Publication number Publication date
NO20005020D0 (en) 2000-10-05
AR015265A1 (en) 2001-04-18
CA2327688A1 (en) 1999-10-14
NO20005020L (en) 2000-12-06
WO1999051549A1 (en) 1999-10-14
US6048816A (en) 2000-04-11
EP1073614A1 (en) 2001-02-07
JP2002510660A (en) 2002-04-09
AU3379599A (en) 1999-10-25
ID29381A (en) 2001-08-30
AU764570B2 (en) 2003-08-21
EP1073614A4 (en) 2002-06-05
MX213108B (en) 2003-03-05
MXPA00009796A (en) 2001-05-01

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B08K Patent lapsed as no evidence of payment of the annual fee has been furnished to inpi [chapter 8.11 patent gazette]

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